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CO2 Mass Frac ETOH I-BUOH OLEYLOH WATER N4C6 CO2 659.7361 0.005398 0.053978 0.866653 0.071971 0 2.03E-25 2.03E-25 0.001999 1.03E-31 Temperature C. Pressure atm Vapor Frac Mole FloW kmol/hr Mass FloW kg/hr Volume FloW l/hr Enthalpy MMBtu/hr Mass FloW kg/hr ETOH I-BUOH OLEYLOH 0.0053202 WATER 36975.371 N4C6 9.2783454 CO2 57.696326 Mass Frac ETOH 0.0856245 I-BUOH 0.0940682 OLEYLOH 1.18E-07 WATER 0.818824 N4C6 0.0002055 CO2 0.0012777 TABLE 10 25 26 3.18E-26 3.18E-26 659.73611 659.7329 423.46358 0.0597574 0.4237884 0.0004165 0.0312577 0.4773982 0.0073818 102.5 1.04 0 277.92 19540.094 26906.753 —81.768 1762.5643 17759.234 19.116459 160.15661 0.0197013 2.21E-23 0.0894653 0.901434 0.0009703 0.0081293 1.00E-06 1.12E-27 1.23E-08 0.0001 1.23E-08 0.0001 0.0053978 0.0539784 0.8666533 0.0719712 0 0.454929 0.0019992 0.496625 SimulatedBUOH ColumnTra?'lcandLiquidMass Composition Pro?le Outputs for Example 3. Heat Liquid Vapor Liquid Stage C. atm MJ/hr kghr kg/hr kghr kg/hr 0.9237725 0.0761275 0.9237725 0.0761275 0.017062 1.39E-10 Temper- ature Pressure duty floW floW feed feed 1 59.36128 0.986923 0 51520.418 26191636 45834.123 2 60.12645 0.990448 0 51713.885 31819.326 3 60.25385 0.993973 0 51784.246 32012.794 4 60.2306 0.997497 0 51698.837 32083.155 5 60.43466 1.001022 0 51796.771 31997.745 6 60.39883 1.004547 0 51776.559 32095679 7 60.4211 1.008072 0 51765.873 32075.467 8 60.47596 1.011596 0 49214.802 32064.781 9 66.54937 1.015121 0 39332.283 29513.71 10 83.26737 1.018646 0 38067.089 19631.191 11 88.24657 1.022171 0 38643.249 18365.997 12 89.60918 1.025695 0 39648.378 18942.158 13 91.48175 1.02922 0 41563.434 19947.287 14 95.05938 1.032745 0 44591651 21862.343 15 100.302 1.036269 17882.824 19701.091 24890.56 Mixed Liquid Vapor feed product product 1stliquid 2ndliquid Stage kghr kghr kghr floWkg/hr floWkg/hr 1 0 2 0 3 0 4 0 5 0 6 0 7 0 0 26191.636 0 0 0 0 0 0 0 0 0 0 0 0 43926.473 7593.945 50451673 1262.212 50498.203 1286.044 44052646 7646.19 50517.359 1279.412 44098.498 7678.061 44001.078 7764.795 US 8,563,788B2 TABLE 9-c0ntinued Simulated Stream Outputs for Example 3. OLEYLOH 2859956 WATER 23750.5 N4C6 0 6.28E-20 6.28E-20 0 604.342 27386.38 285976.49 285976.49 2859956 1.84E-07 23567.137 23567.137 23750.5 23.3043 23.895623 1793.1255 1.03E-31 48 49 50 60 35 1 0 2204.166 45578.22 48033624 —597.126 35 1 0 165.569 11436.909 15993.984 —42.375 685607115 4862.20184 4.77912468 358625109 35 1 0 662.277 45747636 63975.935 —169.499 2742.4285 19448.807 19.116499 1434.5004 3866.5175 4247.8066 58.603933 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 5477.27593 21909.104 846927162 0.05975736 0.42378844 0.00041654 0.03125768 0.47739816 0.00738179 338.77087 0.0597574 0.4237884 0.0004165 0.0312577 0.4773982 0.0073818 Vapor 0.013842 0.017543PDF Image | RECOVERY OF BUTANOL
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